Process and apparatus for manufacturing capsules



Nov. 20, 1951 H. H. BoGlN 2,575,789

PROCESS AND APPARATUS FOR MANUFACTURING CAPSULES Filed Nov. 15, 1948 4 Sheets-Sheet l INVENTOR.

HERMAN H. BOGIN Z'M/wm ATTORNEYS Nov. 20, 1951 H. H. BOGIN 2,575,789

PROCESS AND APPARATUS FOR MANUFACTURING CAPSULES Filed Nov. 15, 1948 A `4 Sheets-sheet z- FIGS.

INVENTOR. HERMAN H. Boem ffm ALM (PML/0 ATTORNEYS Nov. 20, 1951 H, H, BOC-31N 2,575,789

PROCESS AND APPARATUS FOR MANUFACTURING CAPSULES Filed Nov. 15, 1948 4 Sheets-SheetI 3 -f-wx f--q o. S2 LL `L *o CD l l l `-il 1 l l l :1N

i l l l l I t l I l l 2\ l l 1 l l l l (D l I l l I l m l l l l l I l l l I 'I N i 1 N s l l l I l l INVENTOR.

H ERMAN H.BOGIN Mm /MimZu/O ATTORNEYS Nav. 2o, 1951 H, H, BOGIN v2,575,789

PROCESS AND APPARATUS FOR MANUFACTURING CAPSULES Filed Nov. l5, 1948 v 4 Sheets-Sheet 4 INVENTOR.

HERMAN H. BOGIN M BY ATTORNEYS Patented Nov. 20, 1951 Herman -IL- Begin, Detroit, Mich., assigner to Parke, Davis & Company; Detroit, Mich., a corporation of Michigan Application November 15, 19428, Serial No. 60,006

(CL v1825) 7 Claims.

The invention relates to the manufacture of hard-sheel enteric capsules.

This application is a continuation-impart of my application Serial No. 657,073, filed March 25, 1946 now Patent No. 2,491,475 issued December 20,1949 in which I have claimed capsules composed of a novel enteric composition. The present application is more particularly'directed to the method and apparatus for manufacturing such enteric capsules.

As has been pointed out in application Serial No. 657,073, it is desirable to manufacture my new enteric capsules on automatic machines such as have long been in use for the making of nonenteric hard-shell capsules of ordinary gelatin. An automatic capsule making machine which is commercially used onv a large scale is the one described in Colton Patent No. 1,787,777, issued January 6, 1931. However, the enteric capsules of my invention cannot be satisfactorily produced on such a machine without Vreorganization thereof to compensate for the inherently diil'erent properties of the enteric composition from those of ordinary gelatin. The present invention is directed to a new method and an improved apparatus for manufacturing the capsules of my invention and "it is of particular utility because it permits the use of the machine as described in said Colton patent with only a minimum amount of alteration and reorganization. I

In the present state yof the art, hard-shell gelatin capsules are made by immersing previously lubricated pins in a gelatin solution heated to above room temperature. When the pins with the gelatin coating thereon are removed, this coating is preliminarily set to'an extent to prevent the running of the gelatin by slowly rotating the pins while at the-same time lifting them to an elevated platform." During this movement through the surrounding airat room temperature, the gelatin sets sufliciently so that the pins with the Vgelatin coating at the upper ends may remain relatively stationary without unduly changing Vthe wall thicknessof the gelatin. The pins with the substantially set gelatin coatings are then fed through a drying unit Where the moisture is gradually removed with dehumidiiied air at a temperautre lslightly above room temperature.

The enteric capsules of my invention are of a composition which does notbecome set bythe preliminary drying procedure' above described, and it is not possibleltov manufacture ,s atisfac`4 tory 4 enteric capsules in' the conventioiial"'auto matic machine by merely substituting the new composition.

However, I have invented a method for overcoming thisdiiiiculty by providing supplementary means for setting the composition before the coated pins reach the dryingunit. The preferred method which I employ is to utilize a l current of. air at a temperature lower than room temperature and direct the cool air current on the coated pins in the interval between the withdrawal ,of the dipped pins and the feeding of them in to the drying unit.l I have found that excellent` results are obtained if the cool air current is directedinto contact with the composition as' soon as the coated pins have finished their upward rotating motion as above described. The temperature of the cooling air (less than about F.) and the timethe composition is exposed thereto are such as to insure that the composition is set before it may run sufliciently to alter the uniformity of the capsule Walls.

The cooling feature of the process is a very critical' j`step because the enteric material adherling to the pins does not set as rapidly as ordinary gelatin lbut tends to run and produce a capsule with uneven walls. I have found that this coolmay be'conveniently and rapidly accomplished byblowing cool air across the coated pins but'it should be understood that while this is the preferred method of cooling, the invention 'is not limited to' this particular method.

In order to more fully describe my invention, reference l'should be made to the accompanying drawings,l wherein:

Figure 1 is a diagrammatic side elevation of a portion'of the ordinary capsule-making machine "of 'PatentNo 1,787,777 with the cooling aDllaratus added thereto;

1 Figure 2is a transverse vertical section on the line 2`2 of Figures 1 and 4 showing the dipping units:

`Figure 3 is a similar transverse vertical section on al large scale showing the mechanism for elevating and whirling the capsule-carrying pins; l, Y

' Figure 4 is a top plan view showing the location ofthe cooling means, and

. VVFigure 5 vis a perspective view from the side oppositefrom Figurel.

Referring now to the drawings, I have specifically illustrated only those portions of the capsule-makingmachine which are functionally related to the mechanism for carrying out the 'present jinventiont f The Y remaining mechanism for thempleteauomatic operation of the machine is fully illustrated and described in Colton Patent No. 1,787,777.,

In general, this machine operates on the prinv ciple of progressively advancing a series of pincarrying elongated bars B, each having a single row of pins P thereon. There are two sets of the pin hare-B; one havingfpins ora sizetto dorm the capsulebodyfand'ithe other of :a size to formthe capsule cap, and these pin bars are respectively advanced through duplicate apparatus upon opi-yi posite sides of the longitudinaleenter of the inachine, as illustrated in Figure2; A'efteii-tliecapf sule portions are separately and simul-taneouslyri formed in the duplicate ;apparatu,Si` they@v re.

'fgthe pins up and in position to be moved laterally out of vthveggroovesE2 onto the bed or table K f-f'lWmansglofftheirocler arms R on the vertical shafts R12 1i Inzaccprdaneewithmy invention, the machine joined together and the completdcasul ..df--j1eaassabovez'describedis provided with supplemenlivered from the machine. For simplicity, only one of the duplicate mechanisms willbe ,dez-1 scribed.

ftaryrfcoolinglmeans and, as specifically shown,

thisom-prisesa hood H arranged above the 'tableKin such a position that the group of bars The pins P, upon which the capsulesmare: ,1.

formed, are first greasedin the greasing unit A Eigure 1) The,individual` bars BY move .length-,- wise in the center of the machine on.a carrier.F (Figure 2) are collected .Y in:v groups G oiiivebars each and movedlaterally with-thepnshanging downward. Each ygroup is then` intermittently advanced, step by step-,according to,.a .predetermined `timing arrangement-,until lit, reaches the dipping.. unit -D- where itmis. positionedv above a .tankflv containingasolution ofcapsulefvforming materialz'atthe proper consistencyr and,tempera. ture. The groupof bars isp-then lowered so kthat the pins dip into the :solution andremain there for a short time tocollect aoatingthereon'after which. the roupis; lifted.: fromv the solution .and moved laterally. into v.an elevating device E. The elevator lifts :the group-,to alhigherleveleand during Y the elevation also` rotates the ,coated pins ,throughl the ,-atrrnosphere.A so :as KVto prevent ,the running of thecomposition. Upon reachingthe upper level, the .group Ofbarsis. in a.v horizontal position withfthe pinsP extending.,v upward and each Vgroup ismoved 1 laterally from Ythe. .elevator upon thebed K ofthe drierunitlC. 'fhegroup then remains vstationaryjntl'iis,,postinllntil the next -groupof barsarrivingfrom theelevator movesthenrstgroup laterallyonthelbed.. This sequence vcontinues. until vfour successive., groups G.1G.2, G3 andGI.areirarranged-sidefby 'sideon Y ,the bede in` the position ,indicatedas', P1'. v'libere-.- uponithe four groupsof. ve .barsv eachraremoved together to the. second position P? onithehedlK, and this *intermittentv movement. continues ,step by step throughVV consecutive, 'positions' QP?, etc. 'throughout this entire drier unitlQQ yll'rom.,tl1i$ `pointon, .the machine,neednot.bedescribedhereL butrasA dis/closedfin Batent No. 1,7 87,1777 -,the .bars B after reaching the far endloffthelmacliine are lowered to the original'leveh. and".pass',back l through the. driertov Vreach ,eventually-he automatic. stripping, .cutting andi capping unit. '.'After the' capsule parts have beenV stripped" from the ,pine-the barsB.v are A.moved out of the stripping .unit `to fthe greasingnnit. ,'A preparatoryto .a .repetition oirvtlie operating cycle. y

' The mechanism for operatingthe various units is fully described in- .Patent q,l\l o. 1',71?-7, 7 77 fand need not be repeatedherel HoWeverftlieflntr- 4mittent. advancement. fi groupsffv ,oi-,pin-

carrying bars to the dippingtank Tislshown in Figure. 2 and the: `same fgure illustratesthe mechanism for. lowering. .the groups; intofthedipe ping tank, withdrawing the coatedpindandmoving tnemlaterany into tneieievatorn." Figures illustrates the immune-,movement 0f the group Qffbare in the two; rotary heed -'Whc'h 65 successively@ moved,flaterallyfzunder :the hoodin @tfdelivered from the elevator passes immediately beneath the same before the coated pins have been allowed to remain stationary for, an-ycappreciable length of time. -Coohair is. supplied .to -theghoodithrougha pipe M andjisrl. directed vby-the hoodinto contactfwith .thecoating onithe pins. Theghood H-ispreerablyof a widthito` embrace .the-fouradjacentegroups of barsgGl, G2, G,and .G4 andisvof vaflengtl'itocover.notcnly thelength of the-,barsfinfthe -rstposition Pl on :the bed ortableyKbut1also tdextend. completely over the four groups of bars in the secondpositionPz.

Inzorder that the-.co o ling,-air' may beellectively -utilizedifor the .setting ,or theycoating without unduly cooling.. other,A parts of theautomatic ma chine, it, isdesirable .tofprov-ide, means ffor` producing, individualfstreams of 'air-@directed into contact withgeach .ofA the. coated Ivins.Y One way for. accomplishing-,this result istol provide the hood -zH-.With-za bottom ,plate Hhaving aseriesv of :aperturesrv zlr-lzfarrangedf in axial alignment with each 'of the-coatedpins beneath;l nthe ,hood. yIf desired, iatllervioussheet .H3 may bev placed over then-bottom.'platento serve;,as-,a ltenand .air cleaner.. m .l

It is preferable to operaterlthefautomatic machinein-.a roomwhere the atmosphere; is maintained atf` constantv ,temperature tand. humidity,

such Vas ,74.-.5. E. Altemperature-and.fl3,-fl7 %A humid- Y lheetemperature o Lthecooling air within the: hood should bebelowi i-for. example 523,521?. onexposure..of.` the coated .pins to the cooling air must be sufcient,:tocomplete vthe-setting of ,thefcoating-,.material.. so that there AWillheno,-siibsta'ntial` change, in .forml duringthe remainder. of-.the .,procesa; including the drying step rwhere the. temperatures.' are raised some.- whatfaboveithemoom temperature. y

InkgenreralV Lhave .foundit preferablelto maintain -Ithefcooling air, incontact, .with (the coated pins for not;@substantially .less-time, .than sixty seconds butalorigerperiod-is not harmful; Thus, :with1711er,Inachne.;l as hereinbef ore described the timing" thefmachine may xbeesuch as `tu deposit 4one groupicf'iive barsofgpin's' everyfteen seconds onethertablefel'.; Sincex `four. of e saidvgrdups Vare position'fPlbefore the fouriunitsgare moved longi- 'tudinally-:f`intou1 position .P21 under the rearfposi.-

subj'eeteditoi thecoolingA airv for a longer total WQ mnuteslwlllelthjflaist group has an4` exposure 75 im," thegcop 1g liriofabout seventy-two'seconds,

Thes'e'times are not necessarily critical but are illustrative.

, The subsequent drying operation in the presence of dehumidiiied air usually takes place on a'successively increasing temperature scale starting at about 76 F. The total drying time before the capsule shells are stripped from the pins and the excess removed by cutting it about forty to forty-live minutes.

The enteric capsules of my invention may be prepared from a solution of a material possessing setting properties, such as gelatin, and a water soluble, alkali metal salt of a partial ester of a polycarboxylic acid and a suitable cellulose ester. The partial ester of a polycarboxylio acid andl a cellulose carboxylate derivatives containing free carboxylA groups is dissolved in an aqueous solution of an alkali metal base to obtain an aqueous solution of the corresponding alkali metal salt of the cellulose ester. Some examples. of the alkaline reagents which I may use for this purpose are sodium bicarbonate, sodium carbonate, potassium carbonate, sodium hydroxide, trisodium phosphate, sodium perborate, potassium hydroxide, lithium hydroxide and lithium carbonate. In making these aqueous solutions containing the salts of the cellulosic esters, I prefer to use just enough alkali to eifect the solution of the ester, as any excess alkali present in the final solution tends to destroy or alter the gelatin; However, if desired, an excess of alkali may be used and the excess alkali present in the vresultant solution neutralized with acid before adding the gelatin; or, the solution may be heated until the pH falls to the proper value. The pH of the solution should preferably be on the acid side and about the same as that of the gelatin itself. The proper amount of alkali to use may be readily determined by a simple test on a small sample or it may be calculated if one knows the percentage of free carboxyl groups present in the cellulosic partial ester.

I next4 add the aqueous gelatin solution to the aqueous solution containing the alkali metal salt of the partial ester of a polycarboxylic acid and a cellulose carboxylate derivative. v The mixture is then heated until a homogeneous viscous aqueous solution is obtained. l

. In carrying out my inventionI usepolycar-V boxylic acid partial esters of cellulose esters of lower aliphatic monocarboxylic acids.v These cellulosic derivatives which contain free carboxylgroups may be made by known methods of preparation, such as those disclosed in United States Patents Nos. 2,093,462 and 2,093,464 and also 2,126,460. For example, celluloseor cellulosic derivatives containing free hydroxyl groups can be reacted with a polycarboxylic acid acylating agent, such as an anhydride of the polycarboxylic acid, in the presence of a base, or in the presenceof a solvent and in the absence of an organic base. These partial esters of the various cellulosic derivatives may be simple esters of polycarboxylic acids or they may be mixed esters wherein more than one kind of polycarboxylic acid group is present. I may use the reaction products of polycarboxylic acid anhydrides with cellulose esters containing free hydroxyl groups capable of combining with the same or different acid anhydride of a polycarboxylic acid to form an ester linkage and also increase the number of free carboxylic acid groups present. Such anhydridesl are, for example, phthalic, succinic and maleic, anhydrides. Examples of cellulose derivatives containing free. hydroxylsin the cellulose partof the'molecule which may be acylated are cellu-'f lose acetate; cellulose propionate, cellulose ace. tate-propionate, cellulose butyrate, etc.

I prefer to use the mixed cellulose esters of aA lower aliphatic monobasic acid and a polybasic acid, such as phthalic acid, with at least one free unesteried carboxylic acid group present in the polybasic acid portions of the molecule, e. g. cellulose-acetate-phthalate, cellulose-propionatephthalate and the like. Free carboxyl groups need not be present in molecular portions to the polycarboxylic acid portion of the molecule butv the ester may have'any free carboxyl content of between about 8 and 15% by weight has been found preferable -in the preparation of my new.

enteric capsules, as capsules prepared from such cellulose derivatives disintegrate rapidly on contact with the alkaline secretions of the intestines and also possess better physical properties such as resilience, etc.

As stated above, I combine an aqueous solution of an alkali metal salt of a cellulose derivative, such as cellulose-acetate-phthalate, with gelatin and use the resultant homogeneous aqueous solution inthe preparation of my new enteric capsules. This homogeneous solution containing the essential ingredients of my new capsules must be an aqueous solution. This is due to the fact that gelatin is insoluble in organic solvents such as alcohol, acetone, ether and like solvents whichV readily dissolve the free carboxylic acid cellulose ester derivatives which I use as starting materials. Conversely, these free carboxylic acid cellulose ester derivatives are not soluble in water whereas gelatin is. Thus it is readily apparent that without rst converting these cellulosic esters to a water-soluble salt it is impossible to obtain a homogeneous mixture of the two components which is suitablev for use in making enteric capsules.

I have found that the gelatin-cellulosic material Weight ratio is a critical factor in the preparation of vmy new enteric capsules. This varises from the fact that a suilicient quantity of a salt of the cellulose derivative must be present in the finished capsule to render it insoluble in the stomach acids but the quantity must not be so great as to prevent the rapid solution of the capsule when it comes in contact with the alkaline secretions of the intestine. The amount of the cellulosicsalt present in the iinal capsule is also limited by the fact that if too much is present the capsule is brittle. Moreover, difliculties are encountered during the manufacture of such capsules Whenever sufficient gelatin is not present to set the material on the pin or mold and thus prevent the material from running. I have found that the best results are obtained by starting with about 4 to 9 parts by weight of gelatin to 1 part by weight of the un-neutralized cellulose derivative. In the case of cellulose-acetatephthalate I lndthat particularly valuable entericcapsules are obtained by starting with aboutV the expression parts by weight can only beV properly applied to the parts by weight of the individual. starting materials ,in the form in which awa-vec:

thexgain :in weightY of the `cellulosic material'due tov neutralizationl is. small, theizparts-zby". weight ofV the salt of thel cellulosie.materialpresent: in the Linishedcapsul'e may be considered to.-be the same as the. partsY by weightiof the-un-neutralized cellulosic materiallused asthe starting material.

The amountofwater which I use inftheprepa.- rationv .ofr the aqueous:- Asolution.: containing the gelatinand. the salt ofthe cellulose derivative dependsitola great) extentonthewall .thickness Vde sired inlthe finished capsule. For instancemf a' thinlwalled capsuler is desired, more Water is used in the .preparation off the solution', Whereas.. if a thickewalled capsule is desired azmo-re. concentrated'or. viscous solution is used. For,A example, I have found when starting with 5.6 partsabyweight of gelatin. and 1 part by weightflof. cellulose-v acetate-phthalate that the aqueous.: solution should have a viscosity of between about. v15.0 to` pendent upon` ther temperatureA of,Y the; aqueous solution of gelatin and salt'of-the cellulosederivative. This factor, however, is maintained fairly constant: sincean appreciabled change izr temperatureris necessaryin.orderitoV produce a small change` in wall thickness and z it is undesirable' from ar practical standpointfto. vary thetemperature over large. ranges. Therefore-whenfrprof ducingV my new capsules on automaticnrachines such as that' describedL in Ui. S; Patent".l No; 1,787,777, the gelatn-cellulosesalt solution-'inthey dipping pans is kept-at a fairly constant temperature between about 951V and 120 E'. and pref# erably in the*neighborhoodofabout'llf F;

While the hard-shell capsules of my invention are usually composed solely of 'an' alkali metal salt of a cellulose derivativeVgelatin and, ifl desired; a coloring-agent, itfis permissible-touncorporate a plasticizer also, provided that the amount is not large enough'to changelthe essential requirements of hardness Aand rigdity'neces- I sarygfor a practical hard-shellcapsule. Thus up to 5% (by weight of the dryV gelatin) ofa plasti-A cizer, such as vglycerine or'propylene glycol may be added, if desired, and .theenteric' properties produced by the incorporationy ofv the cellulose derivative are still-retained .when thecomposition containsthis small proportion of plasticizer.

An example of rthe manufacture of hardeshell entericcapsulesby my inventionis as follows.,

AV finely divided miXtureYconsist-ing of v0.9.6 ,1b.4 ofV sodiumY carbonate monohydrate.v and 6 lbs. of cellulose acetate phthalate (-COOH con.

' tent=10.7%`) isfadded with-stirring .to '361lbs-of Y waterfat 180 F'. Inorderto vreduce, frothingioff the mixture', a small amountofLglycerol oleate.

(112'fuid oz.) "may befadd'ed.; AftensolutionisA 7S entericfcapsule Wliclr connipris'eslnii-xfing'f arnaques2V completethe mixtureis allcwedlto'zcool'and stand' overnight. The pH of this solution is.5.9i0-1I;.

VInia :separatacontainer Bllbs; .ofi csseingel'atln (Bloom 25.051 gms)V is.. soakeclfinzwater until .theI mass weigl'lsiz.v llos.y Thea'gelatin is4 removed,Y melted 'atfl40B'Ri andzaddecl with rapidstirring: tether sodiumlsalt or cellulosesacetateephthalate solution. ('IfY a colored..capsule isdesired* aboutV 31/2 oz. of dye are stirred into thefsolutionzat this points?) VThe:resultant solutionis. heatedkat1l12`0 E." forfour tctwelve .'hoursto. insure .homogeneity ofi-` the solution..- Afteria. homogeneousfsolutionfis'- obtained; thes'olutionzis:placedsin' azdippingffpan.

andmaintainediatfa :temperatureoff I 15fi Fi whilea previously lubricatedlpinsr or.' molds are. dipped' inta the. solution'.- v'Iliezpins are'withdrawn and: t

` to' thejbpins totset its` The. capsulehalvesfthus formed Aare driedswitlrdehumdied. air, trimmed,`

: removediromthe pinssandi'joinedztogether'with- :The: finished.. capsules contain about 1.0% by:

weight; or moisture` and are sufliciently` resilient. to.y resist vcracking r even when.` the opposite wallsI are pressedI together..` Theseicapsulesdo not be, come appreciably more brittleieven when heated? for. hours'r at 90 Eintaniatmosphere havingla relative. humidityv of:V only 25% .v When .these-newcapsulesi: are. placed.v in; cold 'airfsaturated' with Water vapor.` they maintain .their shape'muchf better than: thelgelatinz capsulessused .as controlA samples.... Y Y

While-.fthe inventioni'has.- been described above' inf-connection with the e manufacture.: of enteric capsulesiof' certain -chemicallcompositions itmay also bev advantageously:used-.ormaking capsules oiother materialsfwhi'ch vareslower. than'ordinary gelatin in ythe Atimerequired dto.y set for. gel, such; for example, as low grade gelatin (1.1 efgelatin having subnormal setting-1 time); celluloselacetate phthalate, polyvinyl -alcohoLL- cellulose'V acetate, ethyl Acellulose and Vman-y others.-

' Again', while Il have shown'thef cooling air appliedftolthe capsulelmaterial after the elevating and rotating step, my invention contemplates more broadly thest'ep of-post-dip cooling'inlthe intervarprior to theusual dryinglprocedure.

An important-#feature is-tli'atitl requiresno changefin either structure or operaticin of stand# ard machines used inv the.- manufacture of purev gelatin capsules-l otherthan: the introduction of the-'11 post-dip cooling means to-4 adaptV saidmachines :to themanufacture-of Vcapsules `of other chemical compositions.

What-Iclaim as-my'invention vis s l; Process for the'manufacture-ofz a'hardshell enteric Acapsule which comprises mixing an -aqueous# solution of *gelatin and? an aqueous solution of an' alkali-metal salt of apelycarboxylicfacid partial ester ofacellulosef ester; of a lower aliphatic rnonocarlooxyli'cV acidtto obtain a viscousv homogeneousvaqueoussolution, formingv a portion'-offsaid.viscoussolutienzby means -of a mold intolthe shape ofJ'one-h'alf a capsule at a temperature'ofiover :about .1005 E., cooling the.ma`v terial at a'temperature -ofrzlessfth'an 65 F5, drying' the capsule half withdeliumidied air Aand joining saidy capsulehalf with another similar capsule half "having adiameter: suchifthat the .two/:units telescepeeinto-oneanother. l Y

2LPA Process for thefrmanuf'acture vof a hard-shell ous solution of gelatin and an aqueous solution of an alkali metal salt of cellulose acetate phthalate to obtain a viscous homogeneous aqueous solution, forming a portion of said viscous solution by means of a mold into the shape of onehalf a capsule at a temperature of over about 100 F., cooling the material at a temperature of less than 65 F., drying the capsule half with dehumidiiied air and joining said capsule half with another similar capsule half having' a diameter such that the two units telescope into one another.

3. An apparatus for automatically manufacturing capsules, comprising a receptacle for a solution of capsule forming material, means for heating said solution to a predetermined temperature, a multiple pin mold, means for dipping and withdrawing the pins of said mold into and out of the heated solution in said receptacle to coat said pins, means for drying the coating on said pins after the setting of the same, and means for supercooling the coating on said pins in the interval between said withdrawal and said drying to effect the setting of the capsule material.

4. An apparatus for automatically manufacturing capsules, comprising a receptacle for a solution of capsule forming material, means for heating said solution to a predetermined temperature, a multiple pin mold, means for dipping and Withdrawing the pins of said mold into and out of the heated solution in said receptacle to coat said pins, means for repeatedly inverting said pin molds when Withdrawn from the solution, means for drying the coating on said pins after the setting of the same, and means for blowing cooling air over the coating on said pins in the interval between said Withdrawal and said drying to effect the setting of the same in a diminished time interval.

5. A capsule'making machine comprising a receptacle for the capsule forming material, means for heating said material to a predetermined temperature, a holder for a group of pins, means for dipping said group of pins into said heated material, means for withdrawing said group of pins from said heated material with a coating adhering thereto, an elevated platform, an elevator adapted to rotate said group of pins while lifting the same, means for moving said group of pins laterally from said elevator onto said platform, means for intermittently longitudinally advancing said group cf pins on said platform to a drier, and means for blowing cooling air over said -coated pins while on said platform and prior to said longitudinal advancement.

6. A capsule making machine comprising a receptacle for the capsule forming material, means for heating said material to a predetermined temperature, a holder for a group of pins, means for dipping said group of pins into said heated material, means for withdrawing said group of pins from said heated material with a coating adhering thereto, an elevator adapted to rotate said group of pins while transferring the same to an elevated platform, means for intermittently advancing said group of pins on said platform to a drier, a hood over said platform extending to a point adjacent said elevator, and means for blowing air through said hood over said coated pins.

7. In a capsule making machine, the combination with a mechanism for coating pins with a capsule material and means for transferring the coated pins to a drier, of a capsule setting device comprising meansbetween said dipping mechanism and said drier for blowing air at a temperature about F. over said coated pins.

HERMAN H. BOGIN.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 1,787,777 Colton Jan. 6, 1931 1,978,829 Wilkie Oct. 30, 1934 

